TW200819043A - Fine bubble airlift device - Google Patents
Fine bubble airlift device Download PDFInfo
- Publication number
- TW200819043A TW200819043A TW96119538A TW96119538A TW200819043A TW 200819043 A TW200819043 A TW 200819043A TW 96119538 A TW96119538 A TW 96119538A TW 96119538 A TW96119538 A TW 96119538A TW 200819043 A TW200819043 A TW 200819043A
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- Taiwan
- Prior art keywords
- hose
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- portions
- outer casing
- Prior art date
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- 239000007788 liquid Substances 0.000 claims abstract description 81
- 239000011148 porous material Substances 0.000 claims abstract description 11
- 238000005273 aeration Methods 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 65
- 238000000034 method Methods 0.000 claims description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 18
- 239000001301 oxygen Substances 0.000 claims description 18
- 229910052760 oxygen Inorganic materials 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 14
- 238000009423 ventilation Methods 0.000 claims description 11
- 239000013505 freshwater Substances 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 5
- 230000015572 biosynthetic process Effects 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 239000000758 substrate Substances 0.000 claims description 4
- 229920001187 thermosetting polymer Polymers 0.000 claims description 4
- 238000012546 transfer Methods 0.000 claims description 4
- 230000000717 retained effect Effects 0.000 claims description 3
- 238000007665 sagging Methods 0.000 claims description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 2
- 239000011230 binding agent Substances 0.000 claims description 2
- 239000011159 matrix material Substances 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 229920001169 thermoplastic Polymers 0.000 claims description 2
- 239000004416 thermosoftening plastic Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 58
- 239000003570 air Substances 0.000 description 19
- 238000013022 venting Methods 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 239000012267 brine Substances 0.000 description 5
- 238000009792 diffusion process Methods 0.000 description 5
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 5
- 238000013461 design Methods 0.000 description 4
- 239000004800 polyvinyl chloride Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000006213 oxygenation reaction Methods 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 229920000915 polyvinyl chloride Polymers 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 238000005276 aerator Methods 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 2
- 244000144974 aquaculture Species 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 210000003813 thumb Anatomy 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000003491 array Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004570 mortar (masonry) Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000009372 pisciculture Methods 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/20—Activated sludge processes using diffusers
- C02F3/201—Perforated, resilient plastic diffusers, e.g. membranes, sheets, foils, tubes, hoses
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2312—Diffusers
- B01F23/23124—Diffusers consisting of flexible porous or perforated material, e.g. fabric
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
- B01F23/23231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
Description
200819043 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種用於對液體(且詳言之,池塘中之水) 進行通氣及循環之設備。 【先前技術】 存在用以將氣泡引入至大量液體(通常為水)中之各種裝 置。該等裝置具有許多應用’其涵蓋諸如水產養殖(包括 在受控環境中培養及培育魚類(通常稱為養魚))、廢水管理 及其類似者之領域。其他用途在此項技術中通常為吾人已 知。該等裝i包括a常稱為表面通氣裝置及t升裝置之穿 置。 、 、 此項技術中之表面通氣裝置使用槳輪之形式來攪動其表 面附近之水。此導致周圍空氣之氣泡被截獲於水中,該等 氣泡中之某些被吸收至水中。槳葉進一步迫使經通氣之水 離開裝置且將額外之水吸引向裝置以待通氣。表面通氣機 效率低’從而需要相對於所通氣之水之體積的大量能量輸 入。其亦具有可能需要頻繁維護之若干移動零件。 氣升裝置為吾人所知已有許多年’且本質上藉由在水之 表面下方之一預定深度處向水中供應氣泡而操作。此空氣 中之某些㈣收至水中’此導致水變得較不密集且向表面 升&之上升會導致其循環,此使經通氣之水分散且將 1外之水引向裝置以供通氣。藉由使用一擴散器而在一氣 升^置中對水進行通氣。許多形式之擴散器已存在多年且 、吊匕括夕孔體,空氣或另一氣體(諸如氮氣或氧氣)被 120217.doc 200819043 迫使通過此多孔體。當將擴散器浸沒於水中時,# J 乳體通過 裝置之移動會導致氣泡自孔隙中出現且進入水中。 已知的擴散器包括陶瓷圓頂形擴散器及多孔橡膠軟管。 然而,已發現,圓頂形擴散器難以維護、缺乏耐久性且以 大量生產之製造的成本較高。 已將多孔橡膠軟管用於通氣。然而,現有多孔橡膠軟管 及其他多孔橡膠通氣產品之主要缺陷在於:在水中過一段 固化時期之後,軟管需要高空氣壓力輸送系統,因為橡膠 顆粒在水中不能令人滿意地膨脹,藉此減小了孔隙直徑。 減小孔隙直徑會導致流動阻力增加,且隨著管路在其環境200819043 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION The present invention relates to an apparatus for venting and circulating a liquid (and in particular, water in a pond). [Prior Art] There are various devices for introducing bubbles into a large amount of liquid, usually water. These devices have many applications that cover areas such as aquaculture (including the cultivation and cultivation of fish in a controlled environment (often referred to as fish farming)), wastewater management and the like. Other uses are generally known in the art. These devices include a commonly referred to as the surface venting device and the t liter device. The surface venting device of the prior art uses a paddle wheel to agitate water near its surface. This causes bubbles of the surrounding air to be trapped in the water, and some of the bubbles are absorbed into the water. The paddle further forces the vented water out of the device and draws additional water towards the device for ventilation. Surface ventilators are inefficient' requiring a large amount of energy input relative to the volume of vented water. It also has several moving parts that may require frequent maintenance. Airlift devices have been known to us for many years' and operate essentially by supplying air bubbles to the water at a predetermined depth below the surface of the water. Some of the air (4) is taken into the water', which causes the water to become less dense and rise to the surface & the rise will cause it to circulate, which causes the aerated water to disperse and direct the water outside the device to the device for ventilation . Water is ventilated in a gas lift by using a diffuser. Many forms of diffusers have existed for many years and concealed, and air or another gas (such as nitrogen or oxygen) is forced through this porous body by 120217.doc 200819043. When the diffuser is immersed in water, the movement of the #J emulsion through the device causes bubbles to appear from the pores and enter the water. Known diffusers include ceramic dome-shaped diffusers and porous rubber hoses. However, it has been found that dome-shaped diffusers are difficult to maintain, lack durability, and are expensive to manufacture in mass production. Porous rubber hoses have been used for ventilation. However, the main drawback of existing porous rubber hoses and other porous rubber aeration products is that after a period of curing in the water, the hose requires a high air pressure delivery system because the rubber particles do not expand satisfactorily in the water, thereby reducing Small pore diameter. Reducing the pore diameter leads to an increase in flow resistance, and as the pipeline is in its environment
• 彳得到由可熱成型聚合材料(諸如聚氯乙稀(PVC)及聚乙 藉由將氣泡分散於處於熔融狀• 彳 obtained by thermoformable polymeric materials (such as polyvinyl chloride (PVC) and polyethylene) by dispersing the bubbles in a molten state
則的大小及置放。舉例而言, 烯(PE))所製成之多孔軟管。 態之可熱成型材料中,藉此 本體中,此引起孔隙之不規 某些氣泡可能完全包含於軟 120217.doc 200819043 吕之壁内’或可能僅曝露於壁之—侧,兩種情況皆不產生 孔隙。此外,可能需要將多個氣泡連接在一 成完全穿過軟管之通路,此增加了路徑之阻力。此;^ 皆可引起低效率,此可降低使用此擴散器之氣升器的功 效0 β通常,在水之通氣期間擴散至水中之氣泡的大小可藉由 提供形成有較小或較大之孔隙(較小之孔隙產生較小:氣 泡)的擴散裝置而變動。某些已知之裝置偏愛使用較小之 氣泡,因為較小之氣泡更易於被吸收至水中。然而,出於 以上所描述之原因,用於將細氣泡擴散至水中之許多已知 的裝置係昂貴的或操作效率低。其他已知之裝置偏愛使用 杈大且較粗之氣泡,因為該等氣泡可以較高之速度在水中 行進。 因此,存在對以下一種裝置之需要:該裝置可用於有效 地對大量液體進行通氣,同時利用較不昂貴或較可靠之擴 散裝置,該擴散裝置使氣體充分地吸收至液體介質中。只 【發明内容】 ' 根據本發明,設計一種用於具有底部表面之液體介質 (諸如水)本體之通氣的方法,該方法包含··提供一外殼, 該外殼經調適成浮動於液體介質内;以一距液體介質之表 面的預定第一距離及以一距底部表面的預定第二距離而將 一軟管安裝至外殼中之大體上平行於液體介質之表面的預 定位置,該軟官具有形成於其中之複數個孔隙;以一預定 氣體供應速率而向軟管供應氣體,以便以在淡水中大於約 120217.doc 200819043 4磅氧氣/小時/馬力之標準通氣效率而對液體介質進行通 虱。較佳地,該預定氣體供應速率在約1/10 SCFM/軟管縱 尺/、10 SCFM/軟管縱尺之間,且最佳地在約〇.2 SCFM/軟 管縱尺與1.0 SCFM/軟管縱尺之間。 根據本發明之方法之一實施例,軟管包含以一平行陣列 女置之複數個軟管區段。較佳地,該複數個軟管區段在 幸人官區段平行陣列之中心之間規則地隔開在約丨英吋與5英 吋之間的距離,較佳地在軟管區段平行陣列之中心之間以 、,、勺2英叶之距離規則地隔開。 根據本發明之方法之一較佳實施例,預定第一距離在約 6英吋與48英吋之間,較佳在約29英吋與48英吋之間,且 最佳為至少約36英忖。 根據本發明之方法之另一實施例,預定第二距離為至少 約4央吋,較佳為至少約18英吋,且最佳為至少約μ英 对〇 在一較佳實施例中,標準通氣效率在鹽水中大於約6磅 氧氣/小時/馬力。 在本發明之方法之又一實施例中,該方法以在淡水中大 於約4磅氧氣/小時之標準氧轉移速率來提供液體介質之通 氣。 在本發明之方法之另一實施例中,以在鹽水中大於約6 碎氧氣/小時之標準氧轉移速率而對液體介質進行通氣。 本發明係關於一種用於液體介質中之裝置。該裝置包括 外/V又該外设、纟里調適成浮動於該介質内,使得其頂部部 120217.doc 200819043 分保持於介質之頂部表面上方。外殼具有底部部分及開放 侧部分。該裝置進一步包括一軟管,該軟管大體上平行於 液體介質之表面而附接至外殼之底部部分。軟管具有一形 成有複數個孔隙之壁。該複數個孔隙具有在約〇 〇〇1英忖 與約0.004英吋之間的平均直徑,且在軟管之整個長度中 大體上均勻地隔開。該裝置進一步包括一附接至軟管之氣Then the size and placement. For example, a porous hose made of olefin (PE). In the thermoformable material, in this body, the voids caused by the irregularities may be completely contained in the soft wall or may be exposed only to the side of the wall, neither of which is produced. Porosity. In addition, it may be necessary to connect a plurality of bubbles in a passage that completely passes through the hose, which increases the resistance of the path. This can cause inefficiencies, which can reduce the efficacy of the gas lifter using this diffuser. 0 β Generally, the size of the bubbles that diffuse into the water during the aeration of water can be formed by providing smaller or larger The diffusion device of the pores (smaller pores produce smaller: bubbles) varies. Some known devices prefer to use smaller bubbles because smaller bubbles are more easily absorbed into the water. However, for the reasons described above, many known devices for diffusing fine bubbles into water are expensive or inefficient to operate. Other known devices prefer to use larger and thicker bubbles because they can travel in water at higher rates. Accordingly, a need exists for a device that can be used to effectively vent a large volume of liquid while utilizing a less expensive or more reliable diffusion device that allows the gas to be sufficiently absorbed into the liquid medium. [Invention] According to the present invention, a method for venting a body of a liquid medium (such as water) having a bottom surface is provided, the method comprising: providing an outer casing adapted to float in a liquid medium; The soft body has a predetermined position at a predetermined distance from the surface of the liquid medium and a predetermined second distance from the bottom surface to a predetermined position in the outer casing substantially parallel to the surface of the liquid medium. A plurality of pores therein; gas is supplied to the hose at a predetermined gas supply rate to vent the liquid medium with a standard aeration efficiency of greater than about 120217.doc 200819043 4 pounds of oxygen per hour per horsepower in fresh water. Preferably, the predetermined gas supply rate is between about 1/10 SCFM / hose length / / 10 SCFM / hose length, and optimally at about 〇.2 SCFM / hose length and 1.0 SCFM / between hose longitudinals. In accordance with an embodiment of the method of the present invention, the hose includes a plurality of hose sections disposed in a parallel array. Preferably, the plurality of hose sections are regularly spaced between the center of the parallel array of sturdy sections at a distance of between about 5 inches and 5 inches, preferably in a parallel array of hose sections. The centers are regularly separated by the distance between the 2 and the leaves of the scoop. In accordance with a preferred embodiment of the method of the present invention, the predetermined first distance is between about 6 inches and 48 inches, preferably between about 29 inches and 48 inches, and most preferably at least about 36 inches. guess. In accordance with another embodiment of the method of the present invention, the predetermined second distance is at least about 4 angstroms, preferably at least about 18 inches, and most preferably at least about 10,000 angstroms in a preferred embodiment, standard Ventilation efficiency is greater than about 6 pounds of oxygen per hour per horsepower in the brine. In yet another embodiment of the method of the present invention, the method provides a venting of the liquid medium at a standard oxygen transfer rate of greater than about 4 pounds of oxygen per hour in fresh water. In another embodiment of the method of the invention, the liquid medium is vented at a standard oxygen transfer rate of greater than about 6 pulverized oxygen per hour in the brine. This invention relates to a device for use in a liquid medium. The device includes an outer/V and the peripheral device is adapted to float within the medium such that its top portion 120217.doc 200819043 is retained above the top surface of the media. The outer casing has a bottom portion and an open side portion. The device further includes a hose attached to the bottom portion of the outer casing substantially parallel to the surface of the liquid medium. The hose has a wall formed with a plurality of apertures. The plurality of apertures have an average diameter of between about 1 inch and about 0.004 inches and are substantially evenly spaced throughout the length of the hose. The device further includes a gas attached to the hose
體供應管路及用於向該管路供應氣體以使得該氣體穿過該 管路且進入該軟管之構件。 用於向管路供應氣體之構件可包括一位於液體介質之外 部的鼓風機。該鼓風機可藉由一具有第一末端及第二末端 之可撓性軟管而連接至該管路,該第—末端附接至鼓風機 之出口部分,且該第二末端附接至管路之入口部分。 本發明之另一實施例係針對一種用⑤液體彳質中之裝 置。該裝置包括-外殼’該外殼經調適成浮動於該介質 内,使得其頂部部分保持於介質之頂部表面上方。外殼具 有底部部分及開放侧m裝置進_步包括—附接於外 殼之開放底部部分附近的管路。該管路形成—具有第一侧 :第二側之矩形。複數個軟管部分各具有第一末端及第二 〜該複數個軟管部分之第一末端附接至矩形管路之第 :側’且該複數個軟管部分之第二末端附接至矩形管路之 弟-侧,使得氣體可在複數個軟管部分之 末端處自管路流入複數個軟管 # s ^ °複數個軟管部分中之 母一者進一步具有一形成有複數 隙呈古—a 几1糸之壁’該複數個孔 I有在約〇顧英对與約G刪英呀之間的平均直徑,且 120217.doc 200819043 在軟管之整個長度中大體上均勻地隔開。複數個軟管中之 每一者由分散於熱塑性黏合劑材料之基質内的熱固性聚合 物顆粒形成。該裝置進一步包括用於將氣體供應至管路以 使得該氣體穿過該管路且進入複數個軟管之構件。 本發明之另一實施例係針對一種用於液體介質中之裴 置,其包含:一外殼,該外殼經調適成浮動於該液體介質 内,該外殼具有一開放底部部分、一開放側部分,及具有 一頂端及一底端之複數個侧壁部分,該複數個側壁部分中 之每一者包含一對側壁區段及一介入空間,該空間用於在 該裝置中產生浮力以提供浮動;—軟管,其A體上平行於 介質之表面而附接至外殼之底部部分,且具有一形 數個孔隙之壁,該等孔隙在軟管之整個長度中大體上均勾 地隔開;-氣體供應管路,其附接至基底;及用於向該氣 體供應管路供應m構件。較錢,外殼之底部部分與 複數個側壁部分之底端隔開一預定距離,從而在其間提供 一開放區域。較佳地,該預定距離為約6英吋至24英吋, 更佳為約6英对。 ' 根據該裝置之-實施例,自複數個側壁之頂端至底端之 距離為約18英吋至4英呎,較佳為約18英吋。在一較佳實 施例中’複數個孔隙具有在約請1英时與約請4英^ 間的平均直徑。 在-較佳實施例中’該裝置包括—軟管支樓部件,其安 置於軟管内且延伸其至少整個長度,該軟管支撐部件略微 為剛硬,以便防止該軟管之下垂。 120217.doc -11- 200819043 根據本發明之裝置之另一實施例,軟管包含複數個軟管 I5刀且較佳地,該複數個軟管部分沿外殼之底部部分大 體上均勻地分散。在一較佳實施例中,自複數個軟管部分 中之一者之中心至複數個軟管部分中之一鄰近者的距離為 、、、勺1央对至5夬忖,較佳為約2英对。 ’' 根據本發明之裝置之另一實施例,用於液體介質中之裝 置包含.一外殼,該外殼經調適成浮動於液體介質内,使 得其頂部部分保持於介質之頂部表面上方,該外殼具有一 開放底部部分、一開放側部分,及具有一項端及一底端之 複數個側壁部分;一軟管,其大體上平行於介質之表面而 附接至外殼之底部部分’且具有一形成有複數個孔隙之 壁,該等孔隙在軟管之整個長度中大體上均句地隔開,該 t數個側壁部分中之至少―者包括—用以准許液體介質流 、之開放區域;一翁濟批施;^ 孙 &體供應纽,其附接至基底;及用於 =管路供應氣體之構件。在—較佳實施例中,外殼之底 刀與複數個側壁部分中之至少—者的底端隔開一預定 ::,從而在其中提供開放區域。在一較佳實施例中,該 預疋距離為約6英吋至24英忖, 罢々金 孕乂仫為約6央吋。根據該裝 之一只施例,自複數個側壁之 英 貝為至底端之距離為约18 數個孔㈣古A為約18英4。在—較佳實施例中,複 禮個孔隙具有在約(UKH英时與約〇糊英时之間的平均直 【實施方式】 現參看諸圖(其尹相似的參考數字指代相似的特徵),圖 120217.doc -12- 200819043 1中展示根據本發明之—實施例的裝置Η)。該裝置且有一 包括框架丨4之外殼12。框架14可由任何足夠堅@以切裝 置10之剩餘組件之重量且在存在水(包括鹽水或溶解有廢 料或其他化學物質的水)的情況下將不會腐蝕或另外降解 的材料製成。較佳地,切部件由航海級類似金 屬製成。支撐部件較佳藉由焊接或其他已知方法(包括使 用螺桿、螺釘、鉚釘或其類似者)來組裝。 框架14經結構化以向外殼12提供所要形狀。本文所示之 框架14之結構為矩形稜鏡之形狀,但用於通氣裝置之其他 可接受之形狀(諸如圓柱體)係可能的。熟習此項技術者將 瞭解該等設計以及圖中所示之設計之其他變化的使用。在 圖1及圖2所示之外殼12之設計中,侧壁16附接至框架“之 其右侧1 8、左側20及後側22上。如本文所使用,術語頂 部、底部、左、右、前及後僅為在指代圖中所使用之參考 幾何框架時的方便而使用,且並不意欲限制本發明之範 疇。右侧18、左側20及後側22上之側壁16較佳由一具有類 似於框架14之性質之性質的材料製成,且進一步較佳由航 海級鋁製成。可藉由習知構件(包括螺桿、螺釘、鉚釘、 黏著劑或焊接)而將侧壁16附接至框架14。若使用任何緊 固裝置(諸如螺桿)來將裝置10之各種零件連接在一起,則 該等緊固裝置應由商業級不銹鋼製成。 外殼12之前部28、頂部26及底部30大體上為開放的。此 允許裝置在操作期間自外殼12之底部30吸入水中且經由其 前部28之至少一部分而排出水。下文更詳細地描述該操 120217.doc -13- 200819043 作。然而,有可能包括一固體頂部26,且本發明之利用固 體頂部之一實施例展示於圖7中且在下文加以論述。 參看圖1,柵格32固定於裝置1〇之外殼丨2内之其底部3〇 附近。栅格32包括一管路34及與其進行流體連通之至少一 透氣軟管36。較佳地,軟管36自管路34在一大體上垂直之 方向上突出。進一步較佳地,軟管36在一大體上平行於液 體介質(裝置10用於此液體介質中)之表面的方向上延伸, 但其他配置係可能的。管路34較佳由在存在水(包括鹽水 或溶解有其他化學物質的水)的情況下不會腐蝕或另外降 解的材料製成。適合於管路34之材料之一實例為Pvc,較 佳為航海級PVC。因此較佳的係,管路34相對較剛硬(特別 係與更具可撓性之軟管36相比)。此提供相對較剛硬之氣 體(二氣)供應管線’其將不易於彎曲或扭折。 軟管片段36具有一透氣壁,該透氣壁包括延伸穿過其壁 38且具有在約〇·〇01英吋至約〇 〇〇4英吋範圍内之平均直徑 的複數個微孔。此軟管36較佳為1998年9月22日頒予 M/ic/ze//之美國專利第5,811,164號(’’’164專利,,)中所揭示之 類型’該專利之揭示内容的整體以引用之方式併入本文 中此類型之軟管3 6由熱塑性黏合劑材料基質中之熱固性 聚合物顆粒製成,其可根據描述於,丨64專利中之方法製 成。較佳地’熱固性聚合物顆粒具有約6〇至14〇網格(且更 佳地為約80至1〇〇網格)之網格大小。另外,較佳的係,軟 官36之壁38中之微孔具有至少約8〇%且更佳為至少約9〇0/〇 之均一性。類似軟管之額外變化進一步描述於2006年5月8 120217.doc -14· 200819043 日申明之才示通為 Aeration Device For Use As A Diffuser”且 具有代理人案號TEKNI 3.8-008的同在申請中之美國臨時 專利申請案中,該申請案之揭示内容的整體以引用之方式 併入本文中。 、此外,描述於,164專利中之類型之軟管可進一步經調適 成包括其之一不透氣部分。該部分可通常為沿軟管區段之 長度延伸之縱向條紋的形式。此條紋可由無孔聚合物(諸 如聚乙烯)形成’其可在軟管36之形成期間使用共擠出製 ㈣施加至軟管36。可用於形成條紋37之額外材料為聚氯 乙烯、ABS及聚丙烯。或者’可藉由再溶融軟管本身之多 孔聚合物(藉由.應用具有適當形狀及大小之熱鐵或其類似 者以在需要無孔條紋之位置處再熔融聚合物)來施加條 紋。另外’可在軟管36形成之後藉由塗抹來施加乳谬或類 似材料。*透氣條、紋之寬度較佳在〇1〇英叶與1英吋之 間’㈣為約0·125英对至約0 25英对’且寬度更佳為約 0.25央对。根據軟管之橫向圓周,不透氣條紋可自整個圓 周之⑽動至50%,但較佳地自其之約4%變動至以。* 在本發明之裝置巾❹此類型之形成㈣透氣條紋的軟; 時,可相對於剩餘軟管在向下方向上定向條紋(如圖5辑 不)。此可能為有利的,因為當在該裝置中使 整個圓周周圍透氣之軟管的裝置時,隨著自該軟管之下; ==氣泡及自該軟管之上部部分所發出之氣泡二 過,此等氣泡傾向於聚結。此聚結引起粗泡之 產生’此係不利的。因此,在軟管部分^上包括條紋^可 I20217.doc -15- 200819043 引起較大比例之細泡的產生。 此外,不透氣條紋37可以一偏移方式來定位,如圖几中 所說明。在此配置中,條紋37較佳定位於在任一方向上自 軟管之底部偏移5度與45度之間的點處。藉此,軟管可提 供液體介質之額外定向流動。舉例而言,如圖扑中所說 明,條紋37指向裝置之後部22。此引起較大比例之氣泡產 生於軟管之前部部分(與其後部部分相比),此傾向於將液 體引導至裝置之前部’且傾向於自裝置之後部吸引較多液 體。 已發現’描述於,164專利中之類型之軟管能夠以與一產 生大侍多的氣泡之擴散器所完成之量相當的量來將空氣擴 政至水中,而不需要將更大的功率輸入用於鼓風機。換言 之,’164專利之軟管中存在相對較低量之壓頭損失。此 外,,164專利之擴散軟管與其他已知細泡擴散器相比具有 較低之壓頭損失。此外,已發現’與大氣泡或粗氣泡相 比,每體積空氣之細氣泡更易於被吸收至水中。此增加之 吸收係由於水中之每單位體積之^氣之較小氣泡的^面積 增加。增加之表面積增加了空氣至水中之吸收,因為空氣 僅在氣泡之表面處被吸收至水中。,164專利之擴散軟管之 相對較低的麼頭損失結合空氣(或其他氣體)至水(或其他液 體)中之高吸收位準導致了軟管之高效率,從而使其特別 適合用作本發明之裝置1G中之軟管36。然而,可使用其他 類型之擴散裝置。 較佳地,柵格32包括附接至較料矩形框架形式之管路 120217.doc -16- 200819043 μ㈣錄軟管部㈣在兩末 端處耦接至管路34,使得流過管路34之氣體可自任一侧進 入軟管36。在圖i所示之特定配置中,管路34經組態為一 矩形,其固定於外殼12之底部30附近,使得其形成一平行 於由外殼U之底部爾形成之平㈣平面。較佳地,拇格 32為約8英吸寬(自右側18至左侧2〇量測)及約4英吸深(自前 部28至後部22量測)。然而,栅格32之大小可根據待通氣 之液體的體積而變動。另外’可能有必要改變較佳尺寸, 以便使栅格32配合於外殼12内。在此配置中,軟管部分% 橫向地跨越管路34自外殼12之左侧18附近延伸至外殼^之 右侧20附近。包括軟管部分36自外殼12之前部職向地延 伸至後部22之配置的額外配置係可能的且將為熟習此項技 術者所瞭解。栅格32亦可包括用於軟管部分^之支撑件 35,以便防止在裝置1〇之使用期間軟管部分^之過度移動 或下垂。較佳地,支樓件35在每一#管部分%之頂部及底 邛上I伸此外,較佳的係,針對軟管部分36之每24英吋 之長度使用至少一支撐件35。 、 較佳使用標準1/2英时之NPT帶刺插件而將軟管部分36附 接笞路3 4 $外’較佳將軟管部分沿管路3 4之長度以自 約1英吋至5英吋且較佳自中心至中心為約2英吋之範圍内 的規則間隔隔開。此外,如圖6所示’可將-内部支撐件 39置放於每-軟管部分%之内部。内部支樓件39可由任一 具有充分剛度以沿軟管部分36之長度為其提供支樓的材料 製成内°卩支撐件39較佳具有一使得其延伸進入配件或其 120217.doc •17- 200819043 /等…構中之長度,軟管部分36藉由該等結構而附接至 栅才。32。目此,内部支撐件39較佳經設定大小以便配合於 軟管部分36與栅袼32之間的所選擇之附著部分内。適合於 内支撐件39之材料包括聚氯乙烯、ABS、不錄鋼、銘或 任何其他具有充分之強度及/或剛度以支撐軟管部分36的 - 材料。此外,儘管圖6中將内部支撐件39展示為圓形,但 額外形狀(包括三角形、正方形或工字__可能的。 φ 圖所示,在本發明之裝置10之一替代實施例中,管 路34’可形成為一延伸超出外殼12之前部28的矩形形狀。在 =配置中,框架14之固定有柵格32,的部分亦可延伸超出外 殼12之前部28之剩餘部分,以便為柵格32,提供支撐。 現返回至圖i及圖2所示之實施例,管路34連接至氣體源 〇、,、#乂么為泵或豉風機之形式。更佳地,氣體源4〇為再 生式鼓風機。另外,較佳的係,氣體源40為不需要使用油 之類型,因為此可導致油行進至軟管部分36中,此可對其 • 造成損壞。在此配置中使用栗或鼓風機向柵格32供應加壓 之周圍空氣,接著將此空氣通過軟管36而擴散至液體介質 中。較佳地,氣體源40以1/10與1〇標準立方英呎/分鐘 • (SCFM)/柵格32中所使用之軟管縱尺之間的速率向軟管部 ,分36供應氣體。更佳地,氣體源4〇以約〇·2與1〇 8以術軟 管縱尺之間的速率向軟管部分36供應氣體,且更佳為以約 0.4至0·5 SCFM/軟管縱尺之速率,且較佳為〇4 scfm/軟管 縱尺之速率。如圖1及圖2所示,氣體源4〇附接至外殼。之 頂部26(諸如藉由支撐支柱41)且在其入口部分“處使用一 120217.doc • 18 - 200819043 可撓性管件44而連接至管路34。可撓性管件料較佳為被稱 為高壓肥化溶液軟管之管件,但其他類型之可撓性管件可 能為適合的。為了提供藉由氣體源4〇之操作而添加至空氣 之任何過剩熱的耗散,可在氣體源之出口部分與可撓性管 • 件44之間附接一金屬管道區段45(圖4)。較佳地,金屬管道 . 區段45具有約2英吋之直徑及1英呎與4英呎之間的長度。 更佳地,金屬管道區段45具有約18英吋之長度。金屬管道 _ 區段可由鍍辞鋼或任何其他類似之金屬製成。若將泵或鼓 風機用作氣體源40,則有必要使泵或鼓風機位於液體介質 之外部,但沒必要將泵或鼓風機附接至外殼12之頂部%。 更確切地,可使泵或鼓風機位於水之外部之任何地方,其 中其可使用可撓性管件44而連接至柵格32之入口部分42。 此外,為了降低來自周圍空氣内之碎屑陷於軟管部分36之 孔隙中的可此性,可與氣體源4〇 一起使用一空氣過濾器 (未圖示)。 籲 浮t 5 0附接至外设12,較佳附接至在其頂部2 6附近的至 少兩側(例如,圖i所示之左側18及右側2〇)上。浮標5〇經設 计且之位於外殼12上,以便使裝置1〇在液體介質内維持於 • 適當位準處。通常,裝置1〇之適當位準使得柵格32在液體 * w貝(裝置10用於此液體介質中)之表面下方約20英吋與55 英寸之間。柵格32相對於液體介質之表面的定位將不僅依 賴於浮標50之定位,而且亦將依賴於外殼12之尺寸。舉例 而曰’在圖1所示之裝置10中,柵格32之垂直中心線在頂 部26下方以大約48英吋之距離隔開,且浮標”在水中之浮 120217.doc -19- 200819043 力中心在外殼12之頂部26下方大約丨英吋處;然而,該等 尺寸可變動。裝置1〇之尺寸(包括框架“之深度及浮標 相對於框架14之定位)應使得才冊格32在液體介質表面^方 約6英叶與48英忖之間,較佳在液體介質表面下方約μ 对與48英忖之間’且最佳在液體介質表面下方至少約36英 对處。此外,裝置10之外殼12不應停置於池塘之底部表面 或該裝置被使用處之其他位置上。 圖1所示之浮標5G為不透氣且不透水之空心圓柱體之形 式;然而’各種其他類型之浮標(包括由泡沫或其類似者 所製成之浮標)係可能的。浮標亦可包括形成於其中之孔 ⑽,該等孔口52由可移除式栓㈣密封。孔口 52允許向 /予軚50中引入水或其他液體,以便調整浮標“之浮力中 心’此允許操縱裝置1()在液體介質内之總體位置。舉例而 言’藉由添加水’浮標50之浮力中心上升’藉此相對於液 體介質之表面而降低裝置1〇。亦已瞭解,& 了實現最大效 能’最佳為將裝置10定位成使得軟管36之柵格32定位於距 裝置10在上方#作之底部表面(諸如湖泊、池塘或貯槽(裝 置10在其令操作)之底部)為約4英对之最小距離處,較佳為 距底部表面為約19英对之最小距離處,且最佳為距底部表 面為、力24央时之取小距離處。浮標5〇之大小及定位將視液 體貝之組合物及裝置1〇之大小與重量而變動。此外,若 有必要,則浮標50可附接至外殻之後部22以提供額外浮 力。 轉至圖7 ’其中展+ γ 士々 不了本备明之裝置1 〇,,的另一較佳實施 120217.doc -20- 200819043 例。在此情況下,以雙重撇號符號所指示之相似的參考數 字對應於圖1中所採用之相同的參考數字。在此情況下, 裝置10"具有一包括框架14"之外殼12”。再次在此情況 下,框架14"之結構為矩形稜鏡之形狀,但再次,用於通 • 氣裝置之其他可接受之形狀(諸如圓柱體)亦係可能的。在 • ®7所示之外殼12,,之設計中,側壁16”附接至框架14"之复 右側18”、左側20"及後側22"上。然而,在此情況下,发 中所示之裝置H)"不包括本文之圖,i所示之實施例中所使用 的浮標50。而是’每一側壁“"且亦可能為頂壁16"包括一 在封式雙壁構造(此在圖7a中可看出),其包括一對侧壁 16a及16b。因此,一空間17"位於該等成對之侧壁與頂壁 之間-亥空間彳含有諸如空氣之氣體以提供裝置(而非浮 標50)之浮動。再次,該等侧壁—"及⑽"較佳由具有類似 於上文關於框架14而論述之性質之性質的材料製成,諸如 ,佳由航海級銘製成。侧壁16a”及16b"中之每一者可因此 ❿ 藉由習知構件(包括螺桿、螺釘、鉚針、黏著劑或焊接)而 附接至棍木14,。若使用任何緊固裝置(諸如螺桿)來將裝置 10之各種零件連接在—起,則該等緊固裝置應由商業級 ’ 不銹鋼製成。 • 如在圖1所不之實施例之情況下,外殼12,,之前部28,,及 底部3 0"大體卜炎日日,A body supply line and means for supplying gas to the line such that the gas passes through the line and enters the hose. The means for supplying gas to the pipeline may include a blower located outside of the liquid medium. The blower can be coupled to the conduit by a flexible hose having a first end and a second end attached to the outlet portion of the blower and the second end attached to the conduit Entrance section. Another embodiment of the invention is directed to a device for use in a liquid enamel. The device includes an outer casing that is adapted to float within the medium such that its top portion remains above the top surface of the media. The outer casing has a bottom portion and the open side m means includes - a conduit attached adjacent the open bottom portion of the outer casing. The conduit is formed - having a first side: a rectangular shape on the second side. a plurality of hose portions each having a first end and a second to first end of the plurality of hose portions attached to a first side of the rectangular conduit and a second end of the plurality of hose portions attached to the rectangle The younger side of the pipeline allows the gas to flow from the pipeline to the plurality of hoses at the end of the plurality of hose sections. # s ^ ° The mother of the plurality of hose sections further has a plurality of gaps formed in the ancient —a a few walls of the wall' The plurality of holes I have an average diameter between about 英 〇 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英 英. Each of the plurality of hoses is formed from thermoset polymer particles dispersed within a matrix of thermoplastic binder material. The apparatus further includes means for supplying gas to the conduit such that the gas passes through the conduit and into the plurality of hoses. Another embodiment of the present invention is directed to a device for use in a liquid medium, comprising: a housing adapted to float within the liquid medium, the housing having an open bottom portion and an open side portion And a plurality of side wall portions having a top end and a bottom end, each of the plurality of side wall portions including a pair of side wall sections and an intervention space for generating buoyancy in the apparatus to provide a float; a hose, the body of which is attached to the bottom portion of the outer casing parallel to the surface of the medium, and has a wall of a plurality of apertures which are substantially equally spaced throughout the length of the hose; a gas supply line attached to the substrate; and for supplying m members to the gas supply line. More expensive, the bottom portion of the outer casing is spaced a predetermined distance from the bottom ends of the plurality of side wall portions to provide an open area therebetween. Preferably, the predetermined distance is from about 6 inches to 24 inches, more preferably about 6 inches. According to the embodiment of the device, the distance from the top end to the bottom end of the plurality of side walls is from about 18 inches to 4 inches, preferably about 18 inches. In a preferred embodiment, the plurality of pores have an average diameter of between about 1 inch and about 4 inches. In the preferred embodiment, the apparatus includes a hose fulcrum member that is mounted within the hose and extends for at least the entire length thereof, the hose support member being slightly stiff to prevent the hose from sagging. 120217.doc -11- 200819043 According to another embodiment of the apparatus of the present invention, the hose comprises a plurality of hoses I5 and preferably the plurality of hose portions are substantially uniformly dispersed along the bottom portion of the outer casing. In a preferred embodiment, the distance from one of the plurality of hose portions to the adjacent one of the plurality of hose portions is , and the spoon 1 is 5 to 5, preferably about 2 English pairs. According to another embodiment of the apparatus according to the invention, the apparatus for use in a liquid medium comprises an outer casing adapted to float within the liquid medium such that a top portion thereof is retained above the top surface of the medium, the outer casing An open bottom portion, an open side portion, and a plurality of side wall portions having an end and a bottom end; a hose attached to the bottom portion of the outer casing substantially parallel to the surface of the medium and having a Forming a plurality of walls of pores that are substantially uniformly spaced throughout the length of the hose, at least one of the plurality of sidewall portions including - an open region for permitting flow of the liquid medium; A Wengji application; ^ Sun & body supply, attached to the base; and for the = pipeline supply gas components. In a preferred embodiment, the bottom knife of the outer casing is spaced apart from the bottom end of at least one of the plurality of side wall portions by a predetermined :: to provide an open area therein. In a preferred embodiment, the pre-twist distance is about 6 inches to 24 inches, and the strike is about 6 inches. According to one embodiment of the device, the distance between the shells of the plurality of side walls and the bottom end is about 18 holes (four) and the ancient A is about 18 inches. In a preferred embodiment, the brevity of the baptism has an average of about (the UKH and the time of the paste) [Embodiment] Referring now to the figures (the reference numerals similar to Yin refer to similar features) Fig. 120217.doc -12-200819043 1 shows a device according to an embodiment of the invention). The device also has a housing 12 that includes a frame cymbal 4. The frame 14 can be made of any material that is sufficiently stiff to the weight of the remaining components of the cutting device 10 and that will not corrode or otherwise degrade in the presence of water, including brine or water in which waste or other chemicals are dissolved. Preferably, the cut member is made of a marine-grade similar metal. The support members are preferably assembled by welding or other known methods including the use of screws, screws, rivets or the like. The frame 14 is structured to provide the desired shape to the outer casing 12. The structure of the frame 14 shown herein is in the shape of a rectangular crucible, but other acceptable shapes (such as cylinders) for the aerator are possible. Those skilled in the art will be aware of the use of such designs and other variations of the designs shown in the figures. In the design of the outer casing 12 shown in Figures 1 and 2, the side wall 16 is attached to the frame "on its right side 18, left side 20 and rear side 22. As used herein, the terms top, bottom, left, The right, front and rear are for convenience only when referring to the reference geometry used in the drawings, and are not intended to limit the scope of the invention. The side walls 16 on the right side 18, the left side 20 and the rear side 22 are preferably preferred. Made of a material having properties similar to those of the frame 14, and further preferably made of marine grade aluminum. The sidewalls can be made by conventional components including screws, screws, rivets, adhesives or welds. 16 is attached to frame 14. If any fastening means, such as a screw, is used to join the various parts of device 10, the fastening means should be made of commercial grade stainless steel. Front portion 28, top 26 of outer casing 12. And the bottom portion 30 is generally open. This allows the device to draw water from the bottom 30 of the outer casing 12 during operation and to drain water via at least a portion of its front portion 28. This operation is described in more detail below. 120217.doc -13- 200819043 However, it is possible to include one The body top 26, and an embodiment of the present invention utilizing a solid top is shown in Figure 7 and discussed below. Referring to Figure 1, the grid 32 is secured adjacent the bottom 3' of its outer casing 丨2. Grid 32 includes a conduit 34 and at least one venting hose 36 in fluid communication therewith. Preferably, hose 36 projects from a conduit 34 in a generally vertical direction. Further preferably, hose 36 Extending in a direction generally parallel to the surface of the liquid medium (in which the device 10 is used in the liquid medium), but other configurations are possible. The line 34 is preferably comprised of water (including saline or dissolved with other chemicals). An example of a material that is not corroded or otherwise degraded in the case of water. An example of a material suitable for the line 34 is Pvc, preferably marine grade PVC. Therefore, preferred, the line 34 is relatively rigid. (especially compared to a more flexible hose 36.) This provides a relatively rigid gas (two gas) supply line that will not be easily bent or kinked. The hose segment 36 has a gas permeable wall. The permeable wall includes a wall 38 extending therethrough and A plurality of micropores having an average diameter ranging from about 1 inch to about 4 inches. This hose 36 is preferably given to M/ic/ze// on September 22, 1998. The type disclosed in U.S. Patent No. 5,811,164, the disclosure of which is hereby incorporated by reference in its entirety herein in its entirety herein in its entirety in Made of thermoset polymer particles, which can be made according to the method described in the '64 patent. Preferably, the 'thermoset polymer particles have a grid of about 6 to 14 inches (and more preferably about 80 to The grid size of the grid is. In addition, preferably, the micropores in the wall 38 of the soft patron 36 have a uniformity of at least about 8% and more preferably at least about 〇0/〇. Additional changes similar to hoses are further described in the same application on May 8, 2006, 120, 217.doc -14 · 200819043, which states that it is Aeration Device For Use As A Diffuser and has agent number TEKNI 3.8-008 In the U.S. Provisional Patent Application, the disclosure of which is hereby incorporated by reference in its entirety herein in its entirety in its entirety in its entirety in its entirety in its entirety in the entire disclosure of a permeable portion. This portion may generally be in the form of a longitudinal strip extending along the length of the hose section. This strip may be formed from a non-porous polymer such as polyethylene which may be coextruded during formation of the hose 36. (d) applied to the hose 36. The additional materials that can be used to form the strips 37 are polyvinyl chloride, ABS, and polypropylene. Or 'a porous polymer that can be remelted by the hose itself (by application having an appropriate shape and size) Hot iron or the like applies streaks by remelting the polymer at a position where no streaks are required. In addition, a mortar or the like can be applied by application after the formation of the hose 36. The width of the gas permeable strip and the grain is preferably between 〇1〇英叶 and 1 inch '[(4) is about 0·125 inches to about 0 25 inches pair and the width is more preferably about 0.25 yang. According to the hose The lateral circumference, the air-impermeable stripe can be moved from the entire circumference (10) to 50%, but preferably from about 4% to the same. * In the device of the present invention, the formation of this type (four) the softness of the breathable stripe; The stripe can be oriented in the downward direction relative to the remaining hose (as shown in Figure 5). This may be advantageous because when the device is used to vent the entire circumference of the hose in the device, Under the tube; = = bubbles and bubbles from the upper part of the hose are two, these bubbles tend to coalesce. This coalescence causes the generation of coarse bubbles 'this is unfavorable. Therefore, in the hose part The inclusion of stripes ^ can be I20217.doc -15- 200819043 causes a large proportion of fine bubbles to be generated. In addition, the air-impermeable stripes 37 can be positioned in an offset manner, as illustrated in the figure. In this configuration, the stripes 37 is preferably positioned at a point offset between 5 and 45 degrees from the bottom of the hose in either direction. Thus, the hose can provide additional directional flow of the liquid medium. For example, as illustrated in the flap, the strips 37 are directed toward the rear portion 22 of the device. This causes a larger proportion of bubbles to be created in the front portion of the hose (with its rear portion) In contrast, this tends to direct the liquid to the front of the device and tends to attract more liquid from the rear of the device. It has been found that the hose of the type described in the '164 patent is capable of producing a large The bubble diffuser accomplishes a considerable amount of air to expand the air into the water without the need to use a larger power input for the blower. In other words, there is a relatively low amount of head loss in the '164 patent hose. . In addition, the diffusion hose of the '164 patent has a lower head loss than other known fine bubble diffusers. Further, it has been found that fine bubbles per volume of air are more easily absorbed into water than large or coarse bubbles. This increased absorption is due to the increased area of the smaller bubbles per unit volume of water. The increased surface area increases the absorption of air into the water because air is only absorbed into the water at the surface of the bubble. The relatively low head loss of the 164 patent diffusion hose combined with the high absorption level of air (or other gas) to water (or other liquid) results in a hose that is highly efficient, making it particularly suitable for use as a hose The hose 36 in the device 1G of the present invention. However, other types of diffusion devices can be used. Preferably, the grid 32 includes a conduit 120217.doc -16 - 200819043 μ (four) recording hose portion (four) coupled to the conduit 34 at both ends such that flow through the conduit 34 Gas can enter the hose 36 from either side. In the particular configuration shown in Figure i, the conduit 34 is configured as a rectangle that is secured adjacent the bottom 30 of the outer casing 12 such that it forms a flat (four) plane parallel to the bottom of the outer casing U. Preferably, the thumb 32 is about 8 inches wide (measured from the right side 18 to the left side 2 inches) and about 4 inches deep (measured from the front 28 to the back 22). However, the size of the grid 32 can vary depending on the volume of liquid to be vented. Additionally, it may be necessary to change the preferred dimensions to fit the grid 32 into the outer casing 12. In this configuration, the hose portion % extends laterally across the conduit 34 from the vicinity of the left side 18 of the outer casing 12 to the vicinity of the right side 20 of the outer casing ^. Additional configurations including the configuration of the hose portion 36 extending from the front portion of the outer casing 12 to the rear portion 22 are possible and will be appreciated by those skilled in the art. The grid 32 may also include a support member 35 for the hose portion to prevent excessive movement or sagging of the hose portion during use of the device. Preferably, the gusset member 35 extends over the top and bottom of each of the tube portions. Further, at least one support member 35 is used for every 24 inches of the length of the hose portion 36. Preferably, the standard 1/2 inch NPT pricking insert is used to attach the hose portion 36 to the manifold. 3 4 Externally, preferably the hose portion is along the length of the conduit 34 from about 1 inch to 5 The miles are preferably spaced apart from the center to the center by a regular interval of about 2 inches. Further, as shown in Fig. 6, the inner support member 39 can be placed inside each of the hose portion. The inner leg member 39 can be made of any material having sufficient rigidity to provide a support for the length of the hose portion 36. The support member 39 preferably has a member such that it extends into the fitting or its 120217.doc • 17 - 200819043 /etc. The length of the structure, the hose portion 36 is attached to the grid by the structures. 32. Thus, the inner support member 39 is preferably sized to fit within the selected attachment portion between the hose portion 36 and the grid 32. Materials suitable for the inner support member 39 include polyvinyl chloride, ABS, unrecorded steel, or any other material having sufficient strength and/or rigidity to support the hose portion 36. Moreover, although the inner support member 39 is shown as being circular in FIG. 6, additional shapes (including triangles, squares, or yokes may be shown in the φ diagram, in an alternative embodiment of the apparatus 10 of the present invention, The conduit 34' can be formed in a rectangular shape that extends beyond the front portion 28 of the outer casing 12. In the configuration, the portion of the frame 14 to which the grid 32 is secured can also extend beyond the remainder of the front portion 28 of the outer casing 12 to The grid 32 provides support. Returning now to the embodiment shown in Figures i and 2, the line 34 is connected to the gas source 〇,,, #乂, in the form of a pump or a blower. More preferably, the gas source 4 Further, preferably, the gas source 40 is of a type that does not require the use of oil, as this can cause oil to travel into the hose portion 36, which can cause damage to it. The pump or blower supplies pressurized ambient air to the grid 32, which is then diffused into the liquid medium through the hose 36. Preferably, the gas source 40 is at 1/10 and 1 inch standard cubic inch per minute. Between the (SCFM)/grid 32 used in the hose longitudinals The rate is supplied to the hose portion, the gas 36. More preferably, the gas source 4 supplies gas to the hose portion 36 at a rate between about 2·2 and 1〇8 at the hose length, and more preferably At a rate of about 0.4 to 0.55 SCFM per hose length, and preferably at a rate of 〇4 scfm / hose length. As shown in Figures 1 and 2, the gas source 4 is attached to the outer casing. The top portion 26 (such as by the support strut 41) and at its inlet portion "is connected to the conduit 34 using a 120217.doc • 18 - 200819043 flexible tubular member 44. The flexible tubular member is preferably referred to as a high pressure. The fitting of the hose of the fertilizer solution, but other types of flexible fittings may be suitable. In order to provide the dissipation of any excess heat added to the air by the operation of the gas source, it may be at the outlet of the gas source. A metal conduit section 45 (Fig. 4) is attached to the flexible tube member 44. Preferably, the metal conduit. Section 45 has a diameter of about 2 inches and is between 1 inch and 4 inches. More preferably, the metal pipe section 45 has a length of about 18 inches. The metal pipe _ section may be plated steel or any other similar gold. If a pump or blower is used as the gas source 40, it is necessary to have the pump or blower outside the liquid medium, but it is not necessary to attach the pump or blower to the top of the outer casing 12%. The pump or blower is located anywhere outside the water, where it can be connected to the inlet portion 42 of the grid 32 using a flexible tubular member 44. Furthermore, in order to reduce debris from the surrounding air from trapping in the pores of the hose portion 36 Alternatively, an air filter (not shown) can be used with the gas source 4 。. The float t 50 is attached to the peripheral 12, preferably attached to at least two sides near its top 26 (for example, on the left side 18 and the right side 2〇 shown in Figure i). The buoy 5 is designed and positioned on the outer casing 12 to maintain the device 1 in the liquid medium at a suitable level. Typically, the proper level of the device 1 is such that the grid 32 is between about 20 inches and 55 inches below the surface of the liquid * w (the device 10 is used in the liquid medium). The positioning of the grid 32 relative to the surface of the liquid medium will depend not only on the positioning of the buoy 50, but also on the size of the outer casing 12. By way of example, in the apparatus 10 shown in Figure 1, the vertical centerline of the grid 32 is spaced about 48 inches below the top 26, and the buoy "floats in the water 120217.doc -19-200819043 force The center is approximately 丨 下方 below the top 26 of the outer casing 12; however, the dimensions may vary. The dimensions of the device (including the depth of the frame and the positioning of the buoy relative to the frame 14) shall be such that the volume 32 is in the liquid. The surface of the media is between about 6 inches and 48 inches, preferably between about μ and 48 inches below the surface of the liquid medium and preferably at least about 36 inches below the surface of the liquid medium. In addition, the outer casing 12 of the device 10 should not rest on the bottom surface of the pond or at other locations where the device is used. The buoy 5G shown in Figure 1 is in the form of a gas-tight and impervious hollow cylinder; however, various other types of buoys (including buoys made of foam or the like) are possible. The buoy may also include apertures (10) formed therein that are sealed by a removable plug (four). The orifice 52 allows water or other liquid to be introduced into/to the crucible 50 to adjust the buoyancy center of the buoy which allows the overall position of the handling device 1 (in the liquid medium). For example, 'by adding water' buoy 50 The buoyancy center rises 'by thereby reducing the device 1' relative to the surface of the liquid medium. It is also understood that & achieving maximum performance 'optimally positioning the device 10 such that the grid 32 of the hose 36 is positioned at a distance from the device 10 is at the bottom of the top surface (such as the lake, pond or sump (the device 10 is at the bottom of its operation)) at a minimum distance of about 4 inches, preferably about 19 inches from the bottom surface. The location is preferably a small distance from the bottom surface and 24 degrees of force. The size and positioning of the buoy 5 变动 will vary depending on the size and weight of the composition and device of the liquid shell. If necessary, the buoy 50 can be attached to the rear portion 22 of the outer casing to provide additional buoyancy. Turning to Figure 7 'where the display + γ can not accommodate the device 1 of the present specification, another preferred implementation 120217.doc -20 - 200819043 Example. In this case, Like reference digital double apostrophe the corresponding symbol indicated in FIG. 1 of the same reference numerals used in this case, the apparatus 10 ". Comprising a frame having a 14 " 12 of the housing. " Again in this case, the frame 14" is in the shape of a rectangular crucible, but again, other acceptable shapes for the gas-passing device, such as cylinders, are also possible. In the design of the outer casing 12 shown in the ®7, the side wall 16" is attached to the right side 18", the left side 20" and the rear side 22" of the frame 14". However, in this case, the device H)" shown in the present invention does not include the buoy 50 used in the embodiment shown in the figure herein. Rather, 'each side wall' "and possibly top wall 16" includes a closed double wall construction (as can be seen in Figure 7a) that includes a pair of side walls 16a and 16b. Thus, a space 17" between the pair of side walls and the top wall - the space containing 空气 contains gas such as air to provide a float for the device (rather than the buoy 50). Again, the side walls - " &(10)" Made of a material having properties similar to those discussed above with respect to frame 14, such as preferably made of marine grades. Each of sidewalls 16a" and 16b" may thus be constructed by conventional components Attached to the stick wood 14 (including screws, screws, rivets, adhesives or welding). If any fastening means, such as a screw, is used to connect the various components of the apparatus 10, the fastening means should be made of commercial grade 'stainless steel. • As in the case of the embodiment of Figure 1, the outer casing 12, the front portion 28, and the bottom portion of the 0"
版上馬開放的。然而,在此情況下,頂部26,,有 可月b包括L 似於上文所論述之側壁16,,之構造的雙壁構 造。然而,在一觖从也 孕父仏實施例中,右側18,,、左側20,,及後側 22上之至少一且| 且季X佳為所有側壁16”包括至少一開放區域 120217.doc -21- 200819043 9、該開放區域接著准許一些水流過該等側壁丨中之一 =或較佳為所有三者。在圖7所示之特定實施例中,至少 一、但較佳為所有側壁16”並不延伸側壁之整個長度或深 ,,但在每一侧壁16,,之底端21”與軟管36”之柵格32"之間 留出一開放區域19"。栅格32”與側壁16"之底部之間的此 開放區域(如由圖7所示之距離χ所表示)或產生於側壁Η,, 中之任何其他位置處的任何其他此開放區域較佳為約6英 吋至24英吋,其中約6英吋之距離為較佳的。此開放區域 之存在准許更多水經過柵格以達成通氣之目的,且進一步 增加了水之定向流動,此在下文加以更全面地論述。 在裝置10之操作中(如圖4中所說明),氣體源(其較佳為 再生式鼓風機之形式)迫使氣體(其較佳為周圍空氣)通過管 件44且進入管路34。接著,氣體流入軟管%,且系統之壓 力增加,直至其達到足以迫使氣體通過軟管36之壁38内之 微孔的位準。此導致在鄰近於軟管36之液體介質内形成大 量小氣泡60。因為氣體與液體介質相比較不密集(此為空 氣擴散至水中之情況),所以氣泡上升離開軟管。隨著繼 續迫使額外空氣進入系統,額外氣泡形成於液體介質中且 上升離開軟管36。液體介質之表面張力導致一些液體介質 氣泡而上升’错此導致液體介質之循環(如圖4中所說 明)。此外,由於氣泡内之一些氣體被吸收至液體中,所 以此經通氣之液體上升至液體之頂部。隨著額外液體向上 升,裝置之頂部附近之水的壓力增加,從而迫使至少一些 水自外殼12之開放前部28流出。 120217.doc -22- 200819043 液體垂直地離開軟管部分36及自裝置10之前部28流出之 移動在軟官部分36下方之液體中產生真空效應,此真空效 應用以將液體自裝置1 〇下方向上吸且吸至軟管部分3 6。本 發明之叙置使足夠之液體(特別為水)循環通過此裝置以自 表面下方至少10英呎處吸引液體,此視液體之性質而定。 此對於大夕數應用(特別為水產養殖及廢水處理)而言綽綽 有餘,因為該等應用中之水深度通常在5英呎與7英呎之 間。The version is open to the horse. However, in this case, the top 26, there is a double wall construction in which the month b includes a configuration similar to that of the side wall 16, discussed above. However, in an embodiment of the parent, the right side 18, the left side 20, and the rear side 22 are at least one and | and the season X is preferably all the side walls 16" including at least one open area 120217.doc -21- 200819043 9. The open area then permits some water to flow through one of the side walls = = or preferably all three. In the particular embodiment shown in Figure 7, at least one, but preferably all of the side walls 16" does not extend the entire length or depth of the side wall, but leaves an open area 19" between the bottom end 21" of each side wall 16, and the grid 32" of the hose 36". This open area between the grid 32" and the bottom of the side wall 16" (as indicated by the distance χ shown in Figure 7) or any other such open area at any other location in the side wall 较佳 is preferred. It is about 6 inches to 24 inches, of which about 6 inches is preferred. The presence of this open area allows more water to pass through the grid for ventilation purposes and further increases the directional flow of water. As discussed more fully below. In operation of apparatus 10 (as illustrated in Figure 4), a gas source, preferably in the form of a regenerative blower, forces gas, preferably ambient air, through tube 44 and Entering line 34. The gas then flows into the hose % and the pressure of the system increases until it reaches a level sufficient to force the gas through the micropores in the wall 38 of the hose 36. This results in a liquid adjacent to the hose 36. A large number of small bubbles 60 are formed in the medium. Because the gas is less dense than the liquid medium (this is the case where the air diffuses into the water), the bubbles rise out of the hose. As the air continues to force additional air into the system, additional The bubble is formed in the liquid medium and rises away from the hose 36. The surface tension of the liquid medium causes some liquid medium bubbles to rise, which in turn causes circulation of the liquid medium (as illustrated in Figure 4). In addition, due to some of the gas within the bubble It is absorbed into the liquid so that the vented liquid rises to the top of the liquid. As the additional liquid rises, the pressure of the water near the top of the device increases, thereby forcing at least some of the water to flow out of the open front 28 of the outer casing 12. 120217.doc -22- 200819043 The movement of the liquid vertically away from the hose portion 36 and out of the front portion 28 of the device 10 creates a vacuum effect in the liquid below the soft portion 36 which is used to draw liquid from below the device 1 Suction up and suck into the hose portion 36. The present invention circulates sufficient liquid (particularly water) through the device to draw liquid from at least 10 inches below the surface, depending on the nature of the liquid. More than enough for large-scale applications (especially for aquaculture and wastewater treatment) because the water depth in these applications is usually 5 inches and 7 inches. Between.
隨著繼續裝置之操作,上升離開軟管部分%及自外㈣ 之前部28流出之液體繼續迫使經通氣之液體離開該裝置。 隨著藉由此循環而產生之真空力繼續吸水使其離開介質之 底部’自液體介質之上表面向下吸引至少一些經通氣之 水。在充分之操作時期(其視介質之體積及裝置ι〇之輸出 而定)之後,整個液體介質可由裝置1〇進行通氣。舉例而 言,根據本發明之一實施例之裝置1〇足以對一含有水且具 有6英吸之平均深度及i英玫至3英故之平均總面積的池塘 進行通氣,其中柵格32包括—具有軟f部分MM英对 X48英吋之矩形管路34,該等軟管部分妬中之每一者且有 -為大約U00英对之直徑,其沿矩形管料之長度以、 吋之間隔(距鄰近軟管36之中心至中心)隔開。 、 可使用如以上所描述之多個裝置或藉由使用—較 ㈣介進行通氣。通常:此 二:置將上具有一栅格’該柵格自前部28至後部22為約48 所描述),但具有-較大寬度,其可高達16英 120217.doc -23 - 200819043 叹。此裝置之外殼12將根據概格3 2之大小之變化而變動 圖7中所說明之裝置10”的操作非常類似於以上關於圖4 所示之裝置而論述的操作。然而,在圖7之裝置J 〇 ”之俨、、兄 下,側壁16”内或下方之開放區域19”的存在增加了水在筆 置ίο”之下部部分中的循環,且因此更多水經過栅格32,,以 達成通氣之目的。此又引起水之定向流動的增加(如圖4所 示),其進一步增加了裝置對整個池塘或隨其之其他水池 進行通氣的能力。此外,使用固體頂壁26"自身可引起麫 通氣之水流出裝置1〇”之前部28”之較大的定向流動。 藉由以上文所論述之方式來利用本發明之裝置,有可能 =遠優於過去可達到之潛能的效率及通氣或充氧潛能來= 得通氣詳5之,藉由控制以上所論述之特定參數,現有 可能在之珂同樣在淡水及鹽水中未見過之位準下獲得該等 增加之效率及通氣潛能。現可在淡水中在切错氧氣^小 時/馬力(例如,鼓風機的)且較佳在約4與約㈣氧氣/小時/ 馬力之間的位準下、且在鹽水中在大於約㈣氧氣/小時/馬 力且較佳在約6與15碎氧氣/小時/馬力t間的位準下獲得標 準通氣效率("SAEwire")作為料參數之量㈣。該等裝置已 (例如)與標準裝置(諸如以上所論述之表面通氣裝置)相比 :效率為其效率之至少兩倍。類似地,如在淡水中以標準 乳轉移速率("贈R”)所量取該等裝置的通氣或充氧潛能 了達成大於4碎氧氣/小時(較佳在約績i㈣氧氣/小時之 間)之SOTR ’且在鹽水中達成大於約㈣氧氣/小時且較佳 在約6與18傍氧氣/小時之間的SOTR。 120217.doc •24- 200819043 〜為了達成該等效率及充氧潛能,再次,以上所論述之特 疋多數在與以上所描述之設備一起使用時可產生該等妗 果。因此,藉由利用一以1/10與10 SCFM/軟管縱尺之間 (較佳在約0.2與1.〇 SCFM/軟管縱尺之間,且更佳在約〇4 與〇·5 SCFM/軟管縱尺之間,且最佳為約〇·4 scfm/軟管縱 尺)之速率向軟管部分輸送氣體的鼓風機;藉由將本發明 之裝置置放成使得軟管安置於液體介質之表面下方約作 料48英奴間,較佳在液體介質之表面下方⑽英忖與 48央吋之間,且最佳在液體介質之表面下方至少約刊英吋 處;藉由將本發明之裝置中之軟管安置於距裝置在上方操 作之底部表面為約4英吋之最小距離處,較佳為距底部表 ^為約18英忖之最小距離處,且最佳為距底部表面為約^ 央吋之距離處;藉由在裝置之側壁中包括開放區域而增加 通過裝置之水流;及藉由利用平行且自每一軟管之中心至 中心隔開約1英吋與5英吋之間(較佳為自中心至中心隔開 約2英吋)的距離之軟管陣列,有可能達成該等高度改良之 結果。 以上針對S ΑΕ及SOTR資料之數字係使用一經認可為其 ASCE標準之非線性回歸技術來計算。 儘皆本文已參考特定實施例而描述了本發明,但應瞭 解,該等實施例僅說明本發明之原理及應用。因此,應瞭 解,可對說明性實施例作出許多修改,且可在不脫離如隨 附申請專利範圍所界定之本發明之精神及範疇的情況下設 計其他配置。 120217.doc -25- 200819043 【圖式簡單說明】 圖1為根據本發明之一實施例之通氣裝置的前部透祝 圖, 圖2為根據本發明之一實施例之通氣裝置的後部透祝 圖; 圖3為根據本發明之一替代實施例之通氣裝置的前部透 視圖;As the device continues to operate, the liquid that has risen away from the hose portion % and from the outer (four) front portion 28 continues to force the vented liquid out of the device. As the vacuum force generated by this cycle continues to absorb water away from the bottom of the medium, at least some of the vented water is drawn downward from the upper surface of the liquid medium. After a sufficient period of operation (depending on the volume of the medium and the output of the device), the entire liquid medium can be vented by the device. For example, a device 1 according to an embodiment of the invention is sufficient to vent a pond containing water and having an average depth of 6 inches and an average total area of i Ying to 3 inches, wherein the grid 32 comprises - a rectangular duct 34 having a soft f-part MM-pair to X-48-inch, each of the hose sections having - a diameter of about U00 inches, which is along the length of the rectangular tube, The spaces are spaced apart from the center to the center of the adjacent hose 36. Ventilation may be performed using a plurality of devices as described above or by using -four. Typically: this two: there will be a grid on the 'the grid from the front 28 to the rear 22 is about 48), but with a - large width, which can be as high as 16 inches 120217.doc -23 - 200819043 sigh. The housing 12 of the device will vary according to the size of the frame 32. The operation of the device 10" illustrated in Figure 7 is very similar to the operation discussed above with respect to the device illustrated in Figure 4. However, in Figure 7 The presence of the open area 19" in or below the side wall 16" of the device J 〇", under the brother, increases the circulation of water in the lower portion of the pen ίο", and thus more water passes through the grid 32, To achieve the purpose of ventilation. This in turn causes an increase in the directed flow of water (as shown in Figure 4), which further increases the ability of the device to vent the entire pond or other pools. In addition, the use of a solid top wall 26" It can itself cause a large directional flow of the venting water out of the device 1"" front portion 28". By utilizing the device of the present invention in the manner discussed above, it is possible = far superior to the potential achievable in the past Efficiency and ventilation or oxygenation potential = ventilating details 5, by controlling the specific parameters discussed above, it is possible to obtain the efficiency of such increases in the same place that is not seen in fresh water and salt water. through Potential. It can now be in fresh water at a level of between 0 hours/horsepower (for example, a blower) and preferably between about 4 and about (4) oxygen/hour/horsepower, and in brine for more than about (four) Oxygen / hour / horsepower and preferably at a level between about 6 and 15 broken oxygen / hour / horsepower t to obtain the standard ventilation efficiency ("SAEwire") as the amount of material parameters (four). These devices have (for example) and Standard devices, such as the surface aerators discussed above, have an efficiency that is at least twice their efficiency. Similarly, such devices are measured at standard milk transfer rates ("R" in fresh water. The aeration or oxygenation potential achieves a SOTR' of greater than 4 clots of oxygen per hour (preferably between about i (four) of oxygen per hour) and achieves greater than about (four) oxygen per hour in the brine and preferably between about 6 and 18 inches of oxygen. SOTR between /hour. 120217.doc •24- 200819043 ~ In order to achieve these efficiencies and oxygenation potential, again, most of the features discussed above can produce such results when used with the devices described above. Therefore, by using between 1/10 and 10 SCFM/hose longitudinal ruler (preferably between about 0.2 and 1. 〇SCFM/hose longitudinal ruler, and more preferably between about 〇4 and 〇·5) a blower that delivers gas to the hose portion at a rate between the SCFM/pipe longitudinals and preferably at a speed of about sc4 scfm/hose; by placing the device of the present invention such that the hose is placed The surface of the liquid medium is about 48 ounces below the surface of the liquid medium, preferably between the surface of the liquid medium (10) inches and 48 吋, and preferably at least about 吋 below the surface of the liquid medium; The hose of the inventive device is disposed at a minimum distance of about 4 inches from the bottom surface of the device being operated above, preferably at a minimum distance of about 18 inches from the bottom surface, and preferably at the bottom. The surface is at a distance of about 吋; the water flow through the device is increased by including an open area in the side wall of the device; and by using parallel and spaced from the center of each hose to the center by about 1 inch and 5 Hose arrays between miles (preferably about 2 inches from center to center) are possible And other highly improved the results. The above figures for S ΑΕ and SOTR data are calculated using a nonlinear regression technique that is recognized as its ASCE standard. The present invention has been described with reference to the specific embodiments thereof, but it should be understood that these embodiments only illustrate the principles and applications of the invention. It is understood that many modifications may be made to the illustrative embodiments, and other configurations may be devised without departing from the spirit and scope of the invention as defined by the appended claims. 120217.doc -25- 200819043 BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a front perspective view of a venting apparatus according to an embodiment of the present invention, and FIG. 2 is a rear view of a venting apparatus according to an embodiment of the present invention. Figure 3 is a front perspective view of a venting device in accordance with an alternative embodiment of the present invention;
圖4為根據本發明之一實施例之通氣裝置的橫截面圖; Θ 5a及圖5b為一軟管部分的橫截面圖,該軟管部分具有 形成於其上之不透氣條紋; 圖6為一軟管部分的橫截面圖,該軟管部分具有一包括 於其中之内部支撐件; 圖7為本發明之一通氣裝置之另一實施例的前部透視 圖;及Figure 4 is a cross-sectional view of a venting apparatus according to an embodiment of the present invention; Θ 5a and 5b are cross-sectional views of a hose portion having air impermeable stripes formed thereon; A cross-sectional view of a hose portion having an inner support member included therein; FIG. 7 is a front perspective view of another embodiment of a venting device of the present invention;
圖7 a為圖7之一部分之側面、部分 【主要元件符號說明】 正視的放大圖。 10 裝置 10,, 裝置 12 外殼 12,, 外殼 14 框架 14,, 框架 16 側壁 16,, 側壁 1202l7.doc -26 - 200819043Fig. 7a is a side view and a part of a portion of Fig. 7. [Explanation of main component symbols] An enlarged view of the front view. 10 device 10,, device 12 housing 12, housing 14 frame 14, frame 16 side wall 16, side wall 1202l7.doc -26 - 200819043
16b,f 側壁 16cn 側壁 17,, 空間 18 右側 18f, 右側 19ff 開放區域 20 左側 20H 左側 21,, 底端 22 後側 22?f 後側 26 頂部 26’, 頂部 28 前部 28,’ 前部 30 底部 30,, 底部 32 拇格 32f 柵格 32,, 栅格 34 管路 34f 管路 35 支撐件 36 軟管 I20217.doc -27- 200819043 36! 軟管 36” 軟管 37 條紋 39 内部支撐件 40 氣體源 41 支撐支柱 42 入口部分 44 可撓性管件16b, f side wall 16cn side wall 17, space 18 right side 18f, right side 19ff open area 20 left side 20H left side 21, bottom end 22 rear side 22? f rear side 26 top 26', top 28 front 28, 'front 30 Bottom 30, Bottom 32 Thumb 32f Grid 32,, Grid 34 Line 34f Line 35 Support 36 Hose I20217.doc -27- 200819043 36! Hose 36" Hose 37 Stripe 39 Internal Support 40 Gas source 41 support post 42 inlet portion 44 flexible pipe fitting
45 金屬管道區段 50 浮標 52 孔口 54 栓塞 60 小氣泡45 metal pipe section 50 buoy 52 orifice 54 plug 60 small bubbles
120217.doc -28-120217.doc -28-
Claims (1)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/478,875 US7622040B2 (en) | 2006-06-30 | 2006-06-30 | Fine bubble airlift device |
| US11/710,857 US7954791B2 (en) | 2006-06-30 | 2007-02-26 | Fine bubble airlift device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW200819043A true TW200819043A (en) | 2008-05-01 |
| TWI380774B TWI380774B (en) | 2013-01-01 |
Family
ID=38668679
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW96119538A TWI380774B (en) | 2006-06-30 | 2007-05-31 | Device for use in a liquid medium and process for aeration of a body of liquid medium |
Country Status (5)
| Country | Link |
|---|---|
| US (2) | US7954791B2 (en) |
| CN (1) | CN103288227A (en) |
| AR (1) | AR061767A1 (en) |
| TW (1) | TWI380774B (en) |
| WO (1) | WO2008005190A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105766775A (en) * | 2016-03-26 | 2016-07-20 | 马翼 | Intelligent aeration equipment based on Internet of Things and used for water aeration |
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| US7954791B2 (en) * | 2006-06-30 | 2011-06-07 | Tekni-Plex, Inc. | Fine bubble airlift device |
| DE202008015792U1 (en) * | 2008-11-28 | 2010-04-15 | Rockbourne Environmental Ltd., Christchurch | Filter system for dirty water |
| US8066873B2 (en) | 2010-03-26 | 2011-11-29 | Kaw Eros G | Floating bioreactor system |
| US20110272831A1 (en) * | 2010-05-04 | 2011-11-10 | Robert Noel Pearson | Wastewater treatment system |
| RU2484023C1 (en) * | 2012-01-11 | 2013-06-10 | Федеральное Государственное Автономное Образовательное Учреждение Высшего Профессионального Образования "Дальневосточный Федеральный Университет" (Двфу) | Apparatus for aerating oil-containing waste water |
| US8512561B2 (en) * | 2012-01-19 | 2013-08-20 | Bader Shafaqa Al-Anzi | Water aerator using a compressed gas container |
| CN102641669B (en) * | 2012-04-30 | 2014-02-19 | 陈怀洲 | Liftable moving aeration device |
| US9475716B2 (en) * | 2012-09-12 | 2016-10-25 | Christopher Scott Keever | Methods for improving liquid quality in a reservoir |
| US9586184B2 (en) * | 2013-10-22 | 2017-03-07 | Medora Environmental, Inc. | Air-powered water circulation systems for ponds, lakes, municipal water tanks, and other bodies of water |
| CN103828759B (en) * | 2014-03-12 | 2016-05-18 | 成都活水源环保科技有限公司 | A kind of oxygen-enriching device moving freely |
| CN104353363A (en) * | 2014-10-14 | 2015-02-18 | 江苏大孚膜科技有限公司 | Aeration branch pipe for membrane assembly |
| CN112850924A (en) * | 2021-02-26 | 2021-05-28 | 厦门烟草工业有限责任公司 | Aeration tank |
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- 2007-02-26 US US11/710,857 patent/US7954791B2/en not_active Expired - Fee Related
- 2007-05-31 TW TW96119538A patent/TWI380774B/en not_active IP Right Cessation
- 2007-06-06 CN CN2013100739875A patent/CN103288227A/en active Pending
- 2007-06-20 WO PCT/US2007/014445 patent/WO2008005190A1/en not_active Ceased
- 2007-06-29 AR ARP070102943 patent/AR061767A1/en active IP Right Grant
-
2011
- 2011-05-25 US US13/115,600 patent/US20110220732A1/en not_active Abandoned
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105766775A (en) * | 2016-03-26 | 2016-07-20 | 马翼 | Intelligent aeration equipment based on Internet of Things and used for water aeration |
| CN105766775B (en) * | 2016-03-26 | 2019-09-03 | 台州金湖机电有限公司 | A kind of intelligent oxygen increasing equipment for oxygenation in water based on Internet of Things |
Also Published As
| Publication number | Publication date |
|---|---|
| AR061767A1 (en) | 2008-09-17 |
| WO2008005190B1 (en) | 2008-03-27 |
| US20080000841A1 (en) | 2008-01-03 |
| TWI380774B (en) | 2013-01-01 |
| US7954791B2 (en) | 2011-06-07 |
| US20110220732A1 (en) | 2011-09-15 |
| CN103288227A (en) | 2013-09-11 |
| WO2008005190A1 (en) | 2008-01-10 |
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